Technical Assignment 3. Mechanical Systems Existing Conditions Evaluation

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Technical Assignment 3 Mechanical Systems Existing Conditions Evaluation The Milton Hershey School New Supply Center Prepared for: William P. Bahnfleth, Ph.D., P.E., Professor Department of Architectural Engineering The Pennsylvania State University Prepared by: Justin Bem November 21 st, 2006

TABLE OF CONTENTS 1.0 EXECUTIVE SUMMARY-----------------------------------------------------------------2 2.0 BUILDING DESIGN BACKGROUND ---------------------------------------------------3 3.0 MECHANICAL SYSTEMS DESIGN OBJECTIVES & REQUIREMENTS --------------------4 3.1 DESIGN INDOOR AND OUTDOOR CONDITIONS -----------------------------5 4.0 MECHANICAL SYSTEMS SUMMARY---------------------------------------------------5 4.1 AIR SIDE MECHANICAL SYSTEM ----------------------------------------------5 4.2 CHILLED WATER SYSTEM -------------------------------------------------------6 4.3 CONDENSER WATER SYSTEM --------------------------------------------------7 4.4 STEAM BOILER AND HOT WATER SYSTEMS ------------------------------------8 5.0 MECHANICAL SYSTEMS CONTROL LOGIC -------------------------------------------8 5.1 TYPICAL SINGLE ZONE AHUs CONTROL LOGIC ------------------------------8 5.2 VARIABLE VOLUME AHUs WITH RETURN FAN CONTROL ---------------------9 5.3 KITCHEN AND BAKERY AHUs--------------------------------------------------10 5.4 VARIABLE VOLUME BOX CONTROL-------------------------------------------10 5.5 45 F CHILLER PLANT CONTROL------------------------------------------------11 5.6 PRIMARY CONDENSER WATER SYSTEM CONTROL ---------------------------11 5.7 STEAM BOILER AND HOT WATER SYSTEM CONTROL -------------------------12 6.0 DESIGN VENTILATION REQUIREMENTS------------------------------------------------12 7.0 DESIGN HEATING AND COOLING LOADS -------------------------------------------14 8.0 ANNUAL ENERGY USE -----------------------------------------------------------------15 9.0 CRITIQUE OF HVAC SYSTEM ----------------------------------------------------------16 9.1 GENERAL SYSTEM CRITIQUE---------------------------------------------------17 9.2 AIR SIDE SYSTEMS CRITIQUE---------------------------------------------------17 9.3 WATER SIDE SYSTEMS CRITIQUE -----------------------------------------------18 10.0 REFERENCES --------------------------------------------------------------------------18 APPENDIX A DESIGN OBJECTIVES DATA -----------------------------------------------19 APPENDIX B HVAC MAJOR EQUIPMENT CHARACTERISTICS --------------------------21 APPENDIX C SYSTEM FLOW DIAGRAMS ------------------------------------------------25 APPENDIX D ANNUAL ENERGY CONSUMPTION AND COST RESULTS -----------------31 Mechanical Systems Existing Conditions Evaluation - 1 -

1.0 EXECUTIVE SUMMARY The Milton Hershey School New Supply Center is a very wide and long single story 110,000 square foot building. Analyzing the existing mechanical systems proves that the design is very practical and energy conscience for this application. However, there are specific features to the HVAC system that have potential for improvements. This document examines the existing mechanical systems and provides in site to areas that need addressed for possible re-design or modifications. The mechanical design engineer for the supply center is H.F. Lenz Company. The engineers set design objectives based on cost and energy saving criteria. Designing the mechanical systems to reach the overall project goal of LEED Certification is the basis of the majority of the engineering tactics used. Integration of other building systems with the HVAC systems is also another very important project goal. Incorporating a condensate water system for rejection of the heat produced from the supply center s large walk-in freezers with the chilled water plant helps reduce the amount of sensible cooling required in those spaces. Using the same boiler plant for HVAC heating for service hot water heating and steam production for process loads also is a major project goal. Carefully planed control logic is also a goal of the project and results in optimal energy efficiency for the HVAC system. Using temperature, humidity, enthalpy, and flow measuring devices with direct digital controls (DDC) as the energy management control system, the HVAC system proves to not only save energy, but also meet the most basic requirement of producing comfortable indoor environments. Even with proper controlling of the HVAC system, alterations or re-designs of the HVAC system may provide cost and energy saving benefits. Areas of the mechanical systems, such as the heat rejection system for the walk-in freezers, need addressed. Incorporating heat recovery systems that will not waste building generated heat has the potential to reduce operating cost. Revaluating the ventilation air systems may mean a significant reduction in the amount of air handling units required for the supply center. First cost savings will result from less material, but energy savings are also a possibility when dedicated outdoor air units are used in replacement of the designed VAV systems. Overall, the design HVAC system is adequate and energy conscience, but there is potential for improvements. Mechanical Systems Existing Conditions Evaluation - 2 -

2.0 BUILDING DESIGN BACKGROUND The Milton Hershey School New Supply Center is a single story 110,000 square foot building with four elevated mechanical mezzanine rooms and contains a variety of spaces. The north and northwest sections of the building consists of general office spaces and conference rooms. Located in the center of the building is the food distribution center for the Milton Hershey School. This area contains large freezers, refrigerators, and temperature controlled storage areas, fifteen in all, totaling to 13,600 square feet to go along with its central food preparation spaces. Aside from the food production section of the building, the New Supply Center also includes a central mail distribution center for the school and a clothing store with an alterations work area. Complementing the four mechanical mezzanine rooms that house the air handling units, a boiler and chiller plant is located on the north side of the building. The east side is mostly loading docks for deliveries, and the south side accommodates a variety of storage space. There are also two data rooms located in the center of the floor plan. Figure one, shown below, gives a breakdown of the space s location in the building as well as the portion of area each occupancy type consumes. Figure 1 Space relationship and area breakdown Mechanical Systems Existing Conditions Evaluation - 3 -

3.0 MECHANICAL SYSTEMS DESIGN OBJECTIVES & REQUIREMENTS The design of the HVAC systems for the Milton Hershey School New Supply Center is based on cost and energy saving criteria. The MEP engineer for the project is H.F. Lenz Company. H.F. Lenz Company s most general goals of the HVAC system design are: o The complete HVAC system shall meet the requirements of the 2003 International Building Code, ASHRAE 62.1-2004 Standard for Indoor Air Quality, and all applicable National Fire Protection Association Standards. o The system will be made as energy efficient as practical in accordance with LEED design principles. Variable volume hydronic pumping and air systems are used where possible. o The amount of rooftop HVAC equipment is minimized as much as possible to ensure good access for maintenance and to maximize equipment life. Along with these goals, the system is designed to integrate other building systems. The central kitchen of the supply center, as explained above, consists of large walk-in freezers and coolers. The walk-in coolers are cooled by fan coil units that are supplied 20 F water from brine chillers. The walk-in freezers are refrigerated by split system DX units using water cooled condensing units. These condensers reject heat to a condenser water loop that is picked up by the HVAC system. A description of the chillers and all other HVAC equipment are located in the following section. Details on the chilled water system are also located in the next section. Integration of other building systems does not just apply to the chilled water system. The HVAC design objectives also include integrating the process heating loads, dishwashers and steam kettles, with the buildings boiler plant. The buildings boiler plant also provides domestic hot water heating along with HVAC hot water. Elaborate kitchen exhaust systems are also required in the project s goals. Incorporating energy saving techniques with the exhaust hoods such as variable speed fans help reduce energy cost. Due to an extensive amount of exhaust air in the food service and loading dock sections of the building, the air side mechanical systems include ventilation make-up air units. The HVAC system, as a whole, generally consists of centrally ducted air handling unit systems. Chilled and hot water systems from the central plant are piped to cooling and heating coils in the AHUs and terminal equipment that both provide the means of conditioning the spaces. Mechanical Systems Existing Conditions Evaluation - 4 -

3.1 DESIGN INDOOR AND OUTDOOR CONDITIONS The design indoor conditions are developed by H.F. Lenz Company and the Milton Hershey School personnel. Collaboration between the two parties results in design heating dry bulb temperatures, cooling dry bulb temperatures, and maximum relative humidity levels for each space. Appendix A includes charts summarizing the design indoor conditions for all occupancy types found in the supply center. The design outdoor conditions used in building simulation models, calculating thermal loads on spaces, and sizing HVAC equipment are found in the ASHRAE Handbook of Fundamentals 2005 (ASHRAE 2005). Since temperature data for Hershey Pennsylvania is not available in the handbook, the design temperatures are from Harrisburg Pennsylvania. Appendix A includes a summary of the design outdoor conditions used in the design of the supply center s HVAC systems. 4.0 MECHANICAL SYSTEMS SUMMARY This section breaks down all of the HVAC systems located in the Milton Hershey School New Supply Center. Each system s equipment characteristics are summarized. 4.1 AIR SIDE MECHANICAL SYSTEM The air side mechanical system for the supply center uses fourteen air handling units. Four of the AHUs are part of multiple zone VAV systems. These air handling units serve offices, dining areas, clothing display and alterations areas, and staff spaces. The air is distributed to these spaces through VAV terminal units with hot water re-heat coils. The perimeter spaces also include fin-tube radiation systems for winter heating. The four VAV air handling units consists of a supply and return fans, 30% and 85% efficient filters, hot water pre-heat and re-heat coils, and a cooling coil. The remaining ten air handling units are single zone spaces that are either part of VAV or CAV systems. However, since they are single zone units, VAV boxes are not used for air distribution to the spaces. All ten AHUs consists of 30% and 85% efficient filters, hot water pre-heat and re-heat coils, cooling coils, and supply fans. Six of the ten single zone AHUs are part of constant volume systems. These units provide make up air for spaces requiring excessive amounts of exhaust (kitchens spaces, loading docks, recycling room). Even though the units operate at 100% outdoor air when the spaces are in operation, the AHUs also have the ability to return air during unoccupied times. The final four single zone air handling units not mentioned are part of VAV systems. These units serve dry storage and Mechanical Systems Existing Conditions Evaluation - 5 -

clothing warehouse areas. The AHUs vary the volume of air supplied at the supply fan via variable frequency drives. The two data rooms located in the center of the building incorporate two systems to provide cooling year round. The data rooms are served by VAV systems, however, when the central VAV air handling unit is operating at an unoccupied mode, ductless split system air conditioners are used to handle the cooling loads. Detailed characteristics on each individual AHU and the split system air conditioner are found in Appendix B. The following figure is a representation of the HVAC air side system zoning plan. Figure 2 Air side mechanical systems zoning plan 4.2 CHILLED WATER SYSTEM The chiller plant of the supply center consists of two (one duty one standby) 270 ton electric driven centrifugal water cooled chillers that produce 45 F water. These chillers are used to meet the normal HVAC building loads. Also included in the chilled water system are two (one duty one standby) water cooled brine Mechanical Systems Existing Conditions Evaluation - 6 -

chillers that produce 20 F water. These chillers service fan coil units located in walk-in-coolers and refrigerated rooms year round. The two sets of chillers in the plant are interconnected in that they all have the capabilities to produce either 45 F or 20 F water for emergency purposes. All four of the chillers operate with R-134a refrigerant and the entire chilled water system (both the HVAC and brine loops) are provided with a 35% propylene glycol solution. As mentioned above, the 45 F water loop also serves two plate frame heat exchangers to pick up the rejected heat from the walk-in freezers. The rejected heat from the freezers is distributed to a condenser water loop. This water loop is then cooled by the chilled water system before returning to the freezer s condensing units. The HVAC chilled water loop incorporates a primary-secondary pumping system. Three primary pumps are located in the chilled water plant and are of a duty-duty-standby configuration. Two secondary pumps with VFDs distribute chilled water to the building loop. A similar pumping configuration is used for the brine loop, however, only four pumps are needed (2 primary, 2 secondary). The chiller room includes a refrigerant leak detection and exhaust system that complies with ASHRAE Standard 15. Detailed characteristics of each chilled water component are found in Appendix B. 4.3 CONDENSER WATER SYSTEM The condenser water system for the chilled water plant includes two induced draft cooling towers for the heat rejection equipment. These service all four of the chiller s condensers. The walk-in freezer s condenser water loop also utilizes the chiller plant s condenser water system. As stated above, the freezer s rejected heat is handled by the HVAC chilled water loop. This operation occurs in the summer months, or when the ambient outdoor temperature is above 50 F. The freezer s condenser water loop bypasses the plate frame heat exchangers that are served by 45 F chilled water and enters a third plate frame heat exchanger served directly by 60 F condensing water from the cooling tower. This process is used for water side free cooling in seasons where the outdoor temperature is below 50 F. The chilled water flow diagram, located in Appendix C, show the three main water loops (condenser water, chilled water, and freezer condenser water). Design temperatures at which each water loop operates is also located on the flow diagram. The freezer s condenser water loop shows the 3-way valve that is used to bypass the chilled water heat exchangers when the system is operating in free cooling mode. Mechanical Systems Existing Conditions Evaluation - 7 -

4.4 STEAM BOILER AND HOT WATER SYSTEMS The boiler plant in the supply center consists of three natural gas-fired fire tube boilers. The two larger boilers, 200 BHP, service the building HVAC heating and domestic water heating loads. The third smaller boiler, 125 BHP, meets the kitchen equipment hot water demands. The boilers also incorporate flue gas recirculation to lower pollution levels. NO X levels are held to 30 parts per million due to this configuration. A combination deaerator and condensate storage tank is used to provide feed water to the boilers. Three active feed water pumps operate continuously with feed water valves located on the boilers. The feed water valves are controlled by level sensors so that minimum water levels are met to avoid potential hazards. As stated above, the steam boilers produce 40 psig steam to service kitchen equipment loads, such as dishwashers. However, hot water for HVAC heating is also produced by these boilers. Hot water is needed to serve fin tube radiators, VAV box reheat coils, and cabinet and horizontal unit heaters. The hot water is produced by conversion of low pressure steam in two (one duty, one standby) shell and tube heat exchangers. Two hot water pumps with VFDs distribute the hot water to the HVAC equipment. Appendix C includes the hot water flow diagram for further illustration of the process. 5.0 MECHANCIAL SYSTEMS CONTROL LOGIC This section includes summaries of the HVAC control systems of operations. Direct digital controls (DDC) are used as the energy management control system for the HVAC equipment in the supply center. 5.1 TYPICAL SINGLE ZONE AHUs CONTROL LOGIC (AHU-9,12-13, and 14) AHU-9, 12, 13, and 14 are operated so that in cooling mode, the cooling coil control valve modulates to maintain a fixed supply temperature of 53 F. When the cooling demand decreases, the supply air fans for the AHUs decrease the quantity of air from the maximum scheduled flow rate to the minimum cooling mode airflow rate (50% of the max cfm). Once the minimum airflow rates are met, the cooling coil control valve decreases the amount of chilled water being supplied to maintain desired space temperatures. When there is a demand for heating, the supply fan operates at the maximum airflow, but the outdoor air damper only allows for the minimum required amount of ventilation air to enter the AHU. The chilled water valve is closed in heating mode, and the heating coil control valve modulates to maintain the desired space conditions. The AHU s supply air temperature is monitored so not to fall below 53 F in heating mode. Mechanical Systems Existing Conditions Evaluation - 8 -

Controlling the ventilation air for these AHUs relies on the DDC system, the outdoor air dampers, and return air dampers. The supply air quantity is measured using a fan-inlet airflow measuring station. The return air quantity is measured using a duct-mounted airflow measuring station. Minimum outdoor airflow rates are controlled by simultaneously modulation the return damper closed and the outdoor air damper open. All devices used in the controlling process are shown in the overall HVAC schematic in Appendix C. Economizer modes for the AHUs are activated by enthalpy controlled systems as seen in the overall HVAC schematic. When the outdoor air enthalpy is less than the return air enthalpy and there is a need for cooling in the space, the return/outdoor air dampers modulate to increase the outdoor airflow and maintain the desired space temperature. When the system is operating at 100% outdoor air and there is still a high cooling demand, the coiling coil control valve modulates to maintain the desired space temperatures. Relative humidity is controlled by the DDC system as well. When space relative humidity rises above the desired upper limit, the AHU operates at the maximum supply air flow rate. The normal temperature control over the cooling coil is overridden, and the control valve is modulated to produce a supply air temperature as low as 51 F to maintain the desired space relative humidity. The reheat coils in the AHUs are then modulated to maintain the desired space drybulb temperature. 5.2 VARIABLE VOLUME AHU WITH RETURN FAN CONTROL (AHU-4, 10) The DDC systems monitors the outdoor air, mixed air, supply air, and return air temperatures and provides a variable supply air temperature as see in the following table. Table 1 Temperature Reset Schedule RETURN AIR TEMPERATURE SUPPLY AIR TEMPERATURE 78 F 51 F 54 F 70 F A rise in supply air temperature means the hot water supply to the heating coil is reduced first. A further rise in supply air temperature then sees modulation of the return and outdoor air dampers until 100% outdoor air economizer mode is activated. A further rise in supply air temperature requires the DDC system to modulate the cooling coil control valve open. As with the single zone AHUs, economizer mode is activated only when the outdoor air enthalpy is lower than return air enthalpy. Mechanical Systems Existing Conditions Evaluation - 9 -

When the outdoor air temperature is above 35 F, the integral face and bypass damper is positioned for full coil flow. The heating coil control valve then modulates to control the discharge air temperature. When the outdoor air temperature is below 35 F, the hot water control valve is positioned for full water flow, and the face and bypass dampers modulate to vary the amount of air passing through the coil. Since these AHUs are variable volume, the DDC system monitors the supply duct static pressures and varies the supply fan speed to maintain 1.05 inches of water gauge. The DDC systems also measure the supply and return air flow rates. Outdoor airflow rates are measured by duct mounted outdoor air flow measuring stations. As with the single zone AHUs, the return and outdoor air dampers are simultaneously modulated to meet the ventilation requirements. The DDC system then modulates the return fan speed to maintain a return air flow rate equal to the supply air flow rate minus the exhaust air flow rates for proper building pressurization. The AHUs with relief fans (AHU-3, 11) instead of return fans operate with similar characteristics as AHU-4 and 10 described above, except relief fan speed is modulated by the DDC to maintain building pressurization. 5.3 KITCHEN AND BAKERY AHUs (AHU-1,2, and 8) The AHUs serving the kitchen and bakery operate with the same temperature control logic as the single zone AHUs. They also include integral face and bypass dampers that operate similarly to the VAV AHUs described above. The ventilation/make-up air quantities are controlled by having the units operate at 100% outdoor air during occupied modes, and the minimum outdoor air flow rates are 5% of the maximum value during unoccupied modes. Controlling the quantities of return and outdoor air is performed similarly as in the single zone AHUs. However, the pressure differential between the kitchen and bakery with the surrounding corridors is monitored and outdoor air flow rates are increased upon increased kitchen negative deferential pressure beyond the set point of -0.02 inches of water gauge. 5.4 VARIABLE VOLUME BOX CONTROL Spaces in the supply center served by VAV systems with terminal boxes with reheat include thermostats for controlling the space temperature. The thermostat monitors the space temperature and modulates the VAV box damper. When the VAV box is operating at minimum air flow and there is still a call for heating, the reheat coil control valve modulates the hot water supply. Mechanical Systems Existing Conditions Evaluation - 10 -

5.5 45 F CHILLER PLANT CONTROL The DDC system provides lead/lag control of both chillers, control over the sequencing of all chilled and condenser water pumps, and control over the loading of the chillers. The DDC system enables the chilled water system whenever the outdoor dry bulb temperature is above 51 F for longer than 15 minutes and any single AHU is energized with the chilled water valve positioned to chilled water flow, or whenever the freezer condensate supply and return systems enters a chilled water mode. The chilled water system is disabled whenever the outdoor temperature falls below 48 F for more than 40 minutes and the condensate water supply and return system is operating in economizer mode (water side free cooling). The chilled water flow diagram, located in Appendix C, illustrates the 3-way control valve that singles to the chillers that the freezer s condensate water system is operating in chilled water mode. The run time of pumps and chillers is logged by the DDC system and the control system automatically provides lead/lag operation for the chillers and lead-lagstandby operation for both the primary chilled water pumps and secondary condenser water pumps. When an accumulated run time of 300 hours is reached for a lead chiller, the control system shall automatically switch the previous lag unit to the current lead unit status until the run hours limit is reached. If a chiller is in operation when the run time limit is reached, the lag unit starts in addition to the lead unit until the lag unit s supply water temperature has time to respond to the chiller starting. The lead unit, at this point, stops and the lead/lag notation now shifts. The flow rate through each chiller s evaporator is measured. Any time the evaporator water flow drops below 50% of the rated flow, the chiller is disabled and an alarm is issued. The DDC system uses the evaporator differential temperature and evaporator water flow to calculate the actual tonnage of refrigeration that is being produced by each chiller. A secondary chilled water flow station determines the total gpm being delivered throughout the secondary (building loop) chilled water piping system. The chilled water flow diagram in Appendix C illustrates these flow measuring devices. Similar control logic is used in the 20 F brine chiller plant as described above. 5.6 PRIMARY CONDENSER WAER SYSTEM CONTROL (COOLING TOWERS) The cooling towers each have a single fan motor controlled through a VFD and they operate in a lead/lag notation. The pumping system is primary secondary with the primary pumps circulating water to the cooling towers. The secondary pumps serve the water cooled chillers and the free cooling heat exchanger in the winter. Mechanical Systems Existing Conditions Evaluation - 11 -

The DDC system monitors the primary condenser water supply temperature. The condenser water system includes an adjustable primary condenser water temperature set point reset configured to the conditions in the following table. Table 2 Condenser Water Temperature Set Point Reset OUTDOOR WET BULB PRIMARY CONDENSER WATER TEMPERATURE 47 F 55 F 72 F 85 F As the chilled water flow diagram illustrates, the economizer, or free cooling, mode of the walk-in freezer s condenser water system involves the bypassing of the chilled water heat exchangers by means of a 3-way valve. When the outdoor air wet bulb temperature falls below 45 F, the economizer mode is activated and the freezer s condenser water loop is diverted to the plate frame heat exchanger handled directly by cooling tower condensing water. When the outdoor air wet bulb temperature is above 52 F, the economizer mode is off. 5.7 STEAM BOILER AND HOT WATER SYSTEM CONTROL The hot water system consists of two steam to hot water converters and two hot water pumps. Each converter (shell and tube heat exchanger) is controlled with two control valves having 1/3 and 2/3 capacities. A temperature sensor is located in the common supply water leaving the heat exchangers and is connected to the DDC system. A proportional plus integral hot water reset control loop is also part of the control system. When the outdoor air temperature is 0 F, the hot water supply temperature is set to 200 F. When the outdoor air temperature is 70 F, the hot water supply temperature is 120 F. The supply water temperature is controlled so that it does not drop below 120 F or exceed 200 F. Hot water flow diagrams, located in Appendix C, further illustrate the hot water control system. Since the Milton Hershey School New Supply Center is currently under construction, there is no operating history of the HVAC systems. 6.0 DESIGN VENTILATION REQUIREMENTS ASHRAE Standard 62.1-2004 Table 6-1 (ASHRAE 2004) provides minimum ventilation rates for breathing zones and governs the design outdoor air requirements of the Supply Center. Table 6-1 includes a list of occupancy categories and the required minimum outdoor air rates per person and per square foot for those spaces. Mechanical Systems Existing Conditions Evaluation - 12 -

The Ventilation Rate Procedure uses a series of equations in conjunction with tables found in Standard 62.1 (ASHRAE 2004) which calculate the amount of ventilation air required for each space based on the it s use, occupancy, and floor area. This procedure then calculates the amount of outdoor air required for each AHU to intake in order to ensure that each space receives at least the minimum amount of outdoor air. Ventilation rates calculated for a compliance check are summarized in Table 3 shown below. The table illustrates the amount of outdoor air each AHU is to intake in order to comply with the standard and the amount of outdoor air each AHU is scheduled to intake according to the design documents provided by H.F. Lenz Company. Table 3 Ventilation Compliance Summary AHU ΣVOZ MAX ZP MIN OA REQ. (VOT CFM) OA SUPPLIED (CFM) COMPLIES WITH STD. 62.1 1 1124 0.1 1124 1150 YES 2 795 0.14 795 1150 YES 3 1957 0.53 3215 3640 YES 4 1817 0.52 3008 5585 YES 5 833 0.26 1041 3000 YES 6 1133 0.30 1416 13500 YES 7 549 0.29 686 3000 YES 8 335 0.09 335 7400 YES 9 943 0.38 1348 1000 NO 10 849 0.51 1414 1125 NO 11 354 0.23 394 1045 YES 12 497 0.19 552 1250 YES 13 896 0.25 996 3000 YES 14 582 0.18 647 800 YES Table 3 shows that two of the fourteen air handlers do not comply with ASHRAE Standard 62.1 2004. The reason for the non-compliance is that the occupancy type assumed for certain areas, such as boys and girls fitting rooms, are assumed retail spaces which differ from the original design. Table 6-1 in Standard 62.1 (ASHRAE 2004) requires 7.5 cfm per person and 0.06 cfm per square foot of ventilation air supplied to these spaces. The original design of the supply center did not use any values on a per person basis. This proves that the original design calculations produced smaller amounts of ventilation air than what Standard 62.1 recommends. There are significant over ventilation results that Table 3 illustrates. Recalling what is mentioned in the control logic section is that these AHUs are 100% outdoor air units for make-up when the kitchen and loading dock areas are in Mechanical Systems Existing Conditions Evaluation - 13 -

operation. The units must provide enough air to meet the thermal loads and to maintain space pressurization. The resulting actual outdoor air flow rate proves to over ventilate the spaces when compared to the value calculated using Standard 62.1. 7.0 DESIGN HEATING AND COOLING LOADS The design heating and cooling are found from the construction documents provided by the H.F. Lenz Company. The equipment schedules on the design documents indicate the peak heating and cooling loads on the coils in each air handling unit. In order to estimate design loads, annual energy consumption, and operating cost of the Milton Hershey School New Supply Center, Carrier s Hourly Analysis Program (HAP) is used as the building energy simulation program. Input data including OA ventilation rates, lights and equipment loads on a W/sq-ft basis, and design occupancy were all taken from design documents that are supplied by H.F. Lenz Company. Table 4 indicates that the computed cooling loads are similar to the design cooling loads. In all but one AHU, the computed load estimates are higher than the design loads. The design heating loads for the supply center are outlined in Table 5. A new natural gas service is proposed to be extended to the new MHS Supply Center facility as the primary source of fuel/ energy. The building heating, domestic water heating, and kitchen equipment is supplied by natural gas. SYSTEM Table 4 Cooling Load Comparison DESIGN COOLING LOAD (FT 2 /TON) COMPUTED COOLING LOAD (FT 2 /TON) DESIGN CW FLOW (GPM) COMPUTED CW FLOW (GPM) AHU-1 67.8 56.1 240.8 253 AHU-2 53.6 40.7 240.8 275.5 AHU-3 378 374.6 57.8 59.91 AHU-4 301 279.0 70.4 74.06 AHU-6 180.7 129 145.3 175.8 AHU-7 389.5 312.4 50.1 47.3 AHU-8 56.2 44.9 79.8 86 AHU-9 516 458.2 38.0 41.2 AHU-10 326 250 40.7 49.3 AHU-11 252 218.9 28.1 38.1 AHU-12 451 381.8 65.8 75.6 AHU-13 325.5 348.2 66.2 51.5 AHU-14 314 313.1 39.1 37.2 Note: AHU-5 does not include a cooling coil - Delivers 100% outdoor air year round Mechanical Systems Existing Conditions Evaluation - 14 -

Table 5 Natural Gas Heating Demand Loads KITCHEN EQUIPMENT 1,820 Building Heating Demand 9,640 Kitchen Domestic Water 3,731 TOTAL STEAM SYSTEM DEMAND 15,191 EQUIPMENT THAT USES GAS DIRECTLY Laundry 800 Clothes 360 Direct Gas For All Cooking 6,828 TOTAL DIRECT EQIUPMENT DEMAND 7,988 TOTAL PEAK DEMAND 23,179 Note: The loads are expressed in equivalent gas input CFH 8.0 ANNUAL ENERGY USE The Hourly Analysis Program is also used to estimate the annual energy consumption for the supply center. Using the same data as in the cooling and heating loads simulation, specifying the mechanical equipment (AHUs, chillers, boilers, cooling towers, pumps, and fans) actually used in the design of the supply center allows for the calculation of annual energy consumption. Performance characteristics, such as efficiencies and COPs, of the major equipment are taken from the design documents supplied by H.F. Lenz Company. The last pieces of information needed to perform a cost estimate are electric utility rates and the cost of natural gas. Meter data or utility bills are not obtainable since the supply center is currently under construction. Therefore, the electricity rates and natural gas cost used in the simulation are from the energy analysis performed by the design engineer (H.F. Lenz Company). Table 6 Energy Rates OFF PEAK DEMAND CHARGE Electric Rates $0.06 / kwh $8.60 / kw Natural Gas Rates $1.35 / therm All airflow rates used in the analysis are taken from the design documents. The load analysis already calculated the design flow rates for each space and that the air handling units supply. Table 7 indicates that the calculated values and the actual design values are very similar. Therefore, these flow rates are used in the simulation. Mechanical Systems Existing Conditions Evaluation - 15 -

Table 7 Supply Air and Outdoor Air cfm/ft 2 Comparison SYSTEM DESIGN SUPPLY AIR (CFM/FT 2 ) COMPUTED SUPPLY AIR (CFM/FT 2 ) VENTILATION SUPPLY (CFM/FT 2 ) AHU-1 3.72 3.72 3.72 AHU-2 4.71 4.71 4.71 AHU-3 0.97 0.96 0.34 AHU-4 1.26 1.25 0.65 AHU-5 1.83 1.81 1.80 AHU-6 1.43 1.43 1.43 AHU-7 0.81 0.80 0.49 AHU-8 4.60 4.60 4.60 AHU-9 0.76 0.75 0.13 AHU-10 1.46 1.45 0.22 AHU-11 1.77 1.75 0.30 AHU-12 0.94 0.93 0.11 AHU-13 1.00 0.99 0.40 AHU-14 1.34 1.33 0.16 Appendix D includes summaries, charts, and figures from the results of the annual energy consumption simulation. Table 8 gives a breakdown of the annual energy cost for operating the HVAC equipment. Table 8 Annual Energy Cost Breakdown COMPONENT ANNUAL COST ($/YR) ANNUAL COST/FT 2 ($/FT 2 YR) % OF TOTAL ENERGY COST HVAC Component Electric 74,337 0.843 9.3 % Natural Gas 32,420 0.368 4.1 % HVAC Subtotal 106,757 1.210 13.4 % Non HVAC Component Electric 64,049 0.726 8.0 % Natural Gas 628,763 7.127 78.6 Non HVAC Subtotal 692,812 7.853 86.6 % TOTAL 799,569 9.063 100 % 9.0 CRITIQUE OF HVAC SYSTEM The Milton Hershey School New Supply Center s mechanical systems are designed with careful attention towards energy conservation and thermal comfort. Overall, the combination of the HVAC systems ability to incorporate other building systems as well as its sophisticated control methods used to minimize energy use while maintaining thermal comfort classifies it as a very good system for this application. The design engineers at H.F. Lenz Company cut no corners in the design, however, there are still alternatives that need addressed. Adjustments to the current design or redesign of certain areas of the Mechanical Systems Existing Conditions Evaluation - 16 -

HVAC system can result in further optimization in first cost, construction cost, and operating cost. 9.1 GENERAL SYSTEM CRITIQUE The supply center is a very wide and long single story 110,000 square foot building. With that said, the design of the air side mechanical system makes perfect sense. The placement of the 14 AHU s on the elevated mezzanine rooms creates neat and organized ductwork runs for each zone. The placement of the boiler and chiller plants also works well for the building lay out. Located at the north side of the building, the building plants are able to distribute hot water, chilled water, and medium pressure steam with little space impact by running piping in the ceiling plenums and up to the mezzanine rooms. As shown in figure 1 and analyzed in Technical Assignment 2, there is a very small percentage of rentable space occupied by the HVAC systems, which creates for an excellent system in this sense. 9.2 AIR SIDE SYSTEMS CRITIQUE Variable air volume and constant air volume systems traditional create humidity problems if not controlled properly. However, as seen in the mechanical systems control logic section (section 5.0), proper air temperature monitoring and modulation of the AHU s cooling and heating coil s control valves creates acceptable indoor air quality. The use of the mezzanine rooms, VAV units, and CAV units opens the doors for possible optimization. Potential energy, initial cost, and construction cost savings will result if dedicated outdoor air systems (DOAS) are used. The use of a DOAS to maintain the space humidity levels and ventilation needs with a parallel system can drastically lower the number of air handling units that are required. The use of another air system is possible for the parallel system, but if a water system is used, this will result in fewer AHUs required. Requiring a lesser amount of air handling units will most defiantly save in first cost, and DOAS are proven to save fan energy. There is potential in construction cost savings in terms of the mezzanine rooms as well. Currently, the elevated mezzanine rooms only house the air handling units and their VFDs. Using outdoor units and locating them on the roof of the supply center means that the elevated mezzanine rooms are not required. Construction and material cost saving potential is now available. Parallel cooling/heating systems are required if DOAS is implemented. This opens the doors for eliminating the use of VAV units, and for finding more energy efficient systems. A water source heat pump system is an option, and the current ductwork layouts will not need major changes. The DOAS creates the need for smaller duct main sizes since only ventilation air is supplied, and the Mechanical Systems Existing Conditions Evaluation - 17 -

correct duct sizes for each zone will not need changing. Only replacement of VAV boxes with the terminal units is required for the system change. The use of a DOAS system with parallel cooling does create maintenance issues. VAV systems are easier to maintain and most facility technicians are more familiar with this design because of its long history. Implementing a heat pump system, for example, creates the potential for additional training of the system operators and more extensive up-keep on the terminal units as compared to VAV boxes. Therefore, the VAV systems originally designed are easily maintained and improving or preserving this category is a challenge. 9.3 WATER SIDE SYSTEMS Recovering the walk-in freezer s rejected heat in the plate frame heat exchangers eliminates the additional cooling load in the kitchen spaces. However, the freezers generate this heat year round and it is basically wasted in the heat exchangers. Heat recovery improvements to this portion of the HVAC systems will ultimately optimize the process. Integrating the water source heat pumps, as stated above, with the freezer condensate water system is an option for heat recovery. Maintaining the loop temperature with the freezer s waste heat instead of a boiler can prove to decrease the size of the boilers scheduled, and ultimately save in fuel consumption. As previously stated, the overall HVAC system is very good, but addressing the issues stated above has the potential to create an even more sustainable system. 10.0 REFERENCES ASHRAE. 2004, ANSI/ASHRAE, Standard 62.1 2004, Ventilation for Acceptable Indoor Air Quality. American Society of Heating Refrigeration and Air Conditioning Engineers, Inc., Atlanta, GA. 2004. H.F. Lenz Company. 2006, Mechanical Construction Documents. H.F. Lenz Company, Johnstown, PA. 2006. H.F. Lenz Company. 2006, HVAC Design Objectives Proposal. H.F. Lenz Company, Johnstown, PA. 2006. Mechanical Systems Existing Conditions Evaluation - 18 -

APPENDIX A DESIGN OBJECTIVES DATA Table A-1 Design Indoor Conditions HEATING DBT ( F) COOLING DBT ( F) MAX % RELATIVE HUMIDITY Main offices 70 74 None (3) Lobby and Office Corridors 70 74 None (3) Public Toilets 70 78 None (3) Servery 70 74 None (3) Dining / Conference 70 74 None (3) Meal Van Loading Dock 60 82 65 Kitchen 70 80 60 Dishwashing 70 80 60 Kitchen Training 70 80 60 Chef's Office 70 74 None (1) Bakery 70 80 60 Bakery Dry Storage 68 78 50 (4) Food Service Offices 70 74 None (3) Kitchen dry goods 68 78 50 (4) Clothing Storage 68 78 None (3) Clothing Shipping / 70 74 None (3) Receiving Used Clothing 70 74 None (3) Alterations 70 74 None (3) Clothing Work Room 70 74 None (3) Clothing Display and 70 74 None (3) Waiting Dry Storage 68 78 50 (4) Bulk Storage / Bulk Staging 68 78 None (3) Staging and staging 68 80 None (1) corridor Transportation Offices 70 74 None (3) Washer / dryer 68 80 None (1) Program Support Inventory 70 (5) 74 (5) None (3) Storage for year round 68 78 None (3) experience Garbage / recycling 50 95 None Receiving and General 68 80 None (1) Building Storage Mail 70 74 None (3) IT Rooms (2) 68 70 None (1) Mechanical / Electrical 60 100 None Rooms Custodial 70 80 60 Break Room 70 74 None (3) Lockers 70 74 None (1) Bread/Bakery Staging 68 80 None (1) Catering Staging 68 80 None (1) Footnotes: (1) No direct, active humidity control is planned but should not rise above 60% RH under normal operating conditions (2) Wintertime humidification may or may not be necessary. Mechanical Systems Existing Conditions Evaluation - 19 -

(3) No direct humidity control is planned, but should not rise above 50% RH under normal operating conditions. (4) Will require a separate de-humidification unit to control humidity. (5) Assumes there will be staff working in this room consistently Note: All of these temperatures are "occupied mode" temperatures (i.e not unoccupied hours). Food storage spaces will not have changes in temperature/humidity requirements according to building occupancy. No humidification systems are anticipated in the building design. The design indoor condition data is supplied by H.F. Lenz Company and designed by H.F. Lenz in conjunction with the Milton Hershey School. Table A-2 Design Conditions for Harrisburg, PA LATITUDE 40.22 Longitude 76.85 Elevation 338 ft Design Summer DBT 92.8 F Design Summer WBT 73.7 F Design Winter DBT 8.3 F Mechanical Systems Existing Conditions Evaluation - 20 -

Quantity APPENDIX B HVAC MAJOR EQUIPMENT CHARACTERISTICS CHILLED WATER SYSTEM EQUIPMENT Centrifugal Water Cooled Chillers Evaporator Compressor Condenser GPM EWT LWT Max Water PD ft Quantity Type NPLV (kw/ton) kw/ton Input GPM EWT Max Water PD ft 2 648 55 45 19.8 1 Centrifugal 0.395 0.627 810 85 22.9 Quantity GPM EWT LWT Water Cooled Brine Chillers Evaporator Compressor Condenser Max Water PD ft Quantity Type Min Cap'y Step kw/ton Input GPM EWT Max Water PD ft 2 155 25.8 20 17.3 2 Screw 10% 1.228 250 85 9.7 Induced Draft Cooling Towers Sump Heaters Quantity Fan CFM EAT WB F LWT F GPM Fan Motor HP VFD? kw V Ph 2 103,700 76 95 85 25 14 480 3 YES Freezer Cond. Closed Loop Plate Frame Heat Exchangers Cold Side Quantity Flow Rate GPM EWT F LWT F Max PD psi Flow Rate GPM Fluid EWT F LWT F Max PD psi Notes 1 135 84 65 2.3 260 Open Loop CDW 60 69.8 8.5 Used for "free" cooling 2 135 84 65 3.5 170.5 Chilled Water 45 60 5.5 Used in summer time operation Air-Cooled Ductless Split System (IT Rooms) Supply OA EAT EAT CFM CFM Nominal Cooling MBH DB WB System EER 559 0 27 80 67 12.1 Mechanical Systems Existing Conditions Evaluation - 21 -

AIR HANDLING UNITS Air Handling Unit Fans AHU Serves Supply Fan Data Return Fan Data CFM OA CFM Ext SP Total SP Drive Type RPM HP BHP VFD? Ext SP Drive Type RPM HP Total SP BHP VFD? 1 Kitchen 22,000 22,000 4 6.18 Belt Plenum 1115 40 31.2 Yes None 2 Kitchen 22,000 22,000 4 6.18 Belt Plenum 1115 40 31.2 Yes None 3 Offices 9,100 3,640 4 5.09 Belt DWDI AF 1846 20 11.5 Yes None 4 Misc Spaces 10,875 5,585 4 5.51 Belt DWDI AF 1122 20 15 Yes 1.87 Belt SWSI FC 700 10 1.87 6.3 Yes 5 Trash Area 3,000 3,000 2 3.28 Belt Plenum 2362 5 3 No None 6 Loading Dock 13,500 13,500 3 5.1 Belt DWDI AF 1123 25 19.3 Yes None 7 Staging 5,000 3,000 3 4.37 Belt Plenum 1769 10 5.9 No 0.85 Belt SWSI FC 562 3 0.85 1.2 No 8 Bakery 7,400 7,400 3 4.64 Belt Plenum 1438 15 8.2 Yes None 9 Dry Storage 6,000 1,000 3 4.78 Belt Plenum 1890 10 7.1 Yes None 10 Clothing 7,500 1,125 4 5.21 Belt Plenum 1510 15 9.4 Yes 0.84 Belt SWSI FC 517 3 0.86 2.2 Yes 11 Misc Spaces 6,145 1,045 4 5.59 Belt Plenum 2006 15 8.6 Yes None 12 Clothing Storage 10,850 1,250 3 4.39 Belt Plenum 1127 20 11.1 Yes None 13 Receiving 7,500 3,000 3 6.15 Belt Plenum 2231 20 11.6 Yes None 14 Dry Storage 6,500 800 3 4.99 Belt Plenum 1977 15 8.1 Yes None Air Handling Units Cooling Coils Chilled Water Coil Hot Water Pre-Heat Coil AHU EAT F LAT F FB Damper SP (in) GPM EWT F #Rows/FPI WPD DB WB DB WB Type EAT F DB LAT F DB SP (in) GPM EWT F #Rows/FPI WPD 1 95 72 51 51 1.02 240.8 45 8/14 11.9 Integ. FB 0 75 0.32 119.1 180 3/12 13.1 2 95 72 51 51 1.02 240.8 45 8/14 11.9 Integ. FB 0 75 0.32 119.1 180 3/12 13.1 3 81.2 64.5 51 51 0.37 57.8 45 6/11 6.5 Integ. FB 39.2 81 0.22 27.5 180 2/12 3.4 4 81.2 64.5 52 51 0.64 70.4 45 8/11 2.2 Integ. FB 39.9 80 0.24 32.1 180 3/6 5.8 5 NONE Integ. FB 48 92 0.32 14.4 180 3/9 0.3 6 95 72 52 52 1.06 145.3 45 8/14 8.7 NONE 33 92 0.17 87.3 180 2/8 7.2 7 87 68.3 51.9 51.8 0.66 50.1 45 8/11 1.7 NONE 60.4 96.3 0.11 19.7 180 1/8 2.5 8 95 72 52 52 0.71 79.8 45 8/14 2.4 Integ. FB 0 79 0.31 42.3 180 3/12 19 9 79.2 64.6 51 51 0.84 38 45 8/11 4.6 NONE 56.7 90 0.14 22.2 180 1/8 3.2 10 74.5 60.6 51.2 50.8 0.43 40.7 45 8/11 2.7 NONE 62.9 98.1 0.11 28.8 180 1/8 2.4 11 75.9 61.4 51 51 0.61 28.1 45 8/14 2.1 NONE 58.1 91 0.15 22.1 180 1/8 3.2 12 78.2 64.1 52 52 0.65 65.8 45 8/11 2 NONE 60.8 97 0.11 43.3 180 1/8 5.9 13 86 69 52 52 1.36 66.2 45 8/14 12.6 Integ. FB 35 74 0.69 21.3 180 2/12 7.1 14 78.4 64.2 52 52 0.95 39.1 45 8/11 4.8 NONE 60.2 91 0.17 22.3 180 1/8 3.2 AHU Air Handling Units Re-heat Coil and Filters Hot Water Re-heat Coil Pre-Filter Data EAT F DB LAT F DB SP (in) GPM EWT F #Rows/FPI WPD Eff % Depth Type Final SP Total Area Sq ft Final Filter Data Eff % Depth Type Final SP Total Area Sq ft 1 52 88 0.15 86.6 180 1/8 6.8 30 2" Flat 0.6 52.08 85 4" Flat 1.2 52.08 2 52 88 0.15 86.6 180 1/8 6.8 30 2" Flat 0.6 52.08 85 4" Flat 1.2 52.08 3 NONE 30 2" Flat 0.6 33.33 85 4" Flat 1.2 33.33 4 NONE 30 2" Flat 0.6 33.33 85 4" Flat 1.2 33.33 5 NONE 30 2" Flat 0.6 11.11 NONE 6 52 87 0.16 52.2 180 1/8 8.4 30 2" Flat 0.6 33.33 85 4" Flat 1.2 33.33 7 52 90.8 0.1 21.3 180 1/8 2.9 30 2" Flat 0.6 15 85 4" Flat 1.2 15 8 52 91 0.1 31.9 180 1/8 2.9 30 2" Flat 0.6 20.83 85 4" Flat 1.2 20.83 9 50 86 0.14 23.6 180 1/8 3.6 30 2" Flat 0.6 15 85 4" Flat 1.2 15 10 NONE 30 2" Flat 0.6 20.83 85 4" Flat 1.2 33.33 11 NONE 30 2" Flat 0.6 15 85 4" Flat 1.2 15 12 52 91 0.11 47 180 1/8 6.9 30 2" Flat 0.6 33.33 85 4" Flat 1.2 33.33 13 52 83 0.21 25.8 180 1/8 3.1 30 2" Flat 0.6 15 85 4" Flat 1.2 15 14 52 86 0.16 24.1 180 1/8 3.7 30 2" Flat 0.6 15 85 4" Flat 1.2 15 Mechanical Systems Existing Conditions Evaluation - 22 -

HOT WATER/STEAM SYSTEM EQUIPMENT Fire Tube Boilers Quantity Fire Rating Gas CFH Gross Output MBH Boiler HP Comb. Air Fan Motor HP Heating Surface Sq Ft/hp Water Volume Gallons 2 8,165 6,695 200 15 5 8,625 1 5103 4,184 125 10 5 5,750 Supply CFM Air-Cooled Ductless Split System (IT Rooms) OA CFM Nominal Cooling MBH EAT DB EAT WB System EER 559 0 27 80 67 12.1 Horizontal Unit Heater (hot water) CFM RPM HP MBH GPM Max PD (ft) 1100 1050 1/30 44.8 5.3 0.23 1050 1050 1/30 37.3 4.4 0.17 450 1550 9 WATT 14.9 1.8 0.014 Cabinet Unit Heater (hot water) CFM MBH GPM PD (ft) # Rows HP RPM 630 41.1 4.9 1.6 1 1/10 1050 430 25.5 3.1 0.61 1 1/10 1050 230 14.1 1.7 0.19 1 1/15 1050 Shell and Tube Heat Exchangers Circulating Fluid (Tubes) Heating Fluid (Shell) Quantity GPM In F Out F PD ft Fluid lbs/hr Press. 2 750 155 180 0.9 Steam 9.544 5 psi Mechanical Systems Existing Conditions Evaluation - 23 -

Pump No Type System CHWP-1 CHWP-2 Flr Mtd Flr Mtd Secondary 45 CHW Secondary 45 CHW Split/Close Coupled? Operation: Duty/Standby? Pumps Fluid Type Max GPM Shut Off HD (ft) Operation Point bhp Max bhp Motor hp RPM VFD? Split Duty Water 1460 115 32 32.8 40 1750 Yes 11" Split Standby Water 1460 115 32 32.8 40 1750 Yes 11" Impeller Diam. CHWP-3 Flr Mtd Primary 45 CHW Split Duty Water 885 44 7 7.6 10 1150 No 10.125" CHWP-3A Flr Mtd Primary 45 CHW Split Duty Water 885 44 7 7.6 10 1150 No 10.125" CHWP-4 Flr Mtd Primary 45 CHW Split Standby Water 885 44 7 7.6 10 1150 No 10.125" CHWP-5 In-Line Primary 20 CHW Close Duty 35% Brine 272 40 2.3 2.8 3 1750 No 6.5" CHWP-6 In-Line Primary 20 CHW Close Standby 35% Brine 272 40 2.3 2.8 3 1750 No 6.5" CHWP-7 CHWP-8 Flr Mtd Flr Mtd Secondary 20 CHW Secondary 20 CHW Split Duty 35% Brine 262 78 4.1 5.1 5 1750 Yes 8.5" Split Standby 35% Brine 262 78 4.1 5.1 5 1750 Yes 8.5" CDWP-1 Flr Mtd Primary Condenser water Split Duty Water 3100 54 24.5 25.8 30 1150 Yes 11.625" CDWP-2 Flr Mtd Primary Condenser water Split Standby Water 3100 54 24.5 25.8 30 1150 Yes 11.625" CDWP-3 In-Line Chiller-1,2 Condenser Water Split Duty Water 1205 51 9.7 10.2 15 1150 No 7.5" CDWP-3A In-Line Chiller-1,2 Condenser Water Split Duty Water 1205 51 9.7 10.2 15 1150 No 7.5" CDWP-4 In-Line Chiller-1,2 Condenser Water Split Standby Water 1205 51 9.7 10.2 15 1150 No 7.5" CDWP-5 In-Line Chiller-3,4 Condenser Water Split Duty Water 390 40 2.7 2.8 3 1750 No 6.5" CDWP-6 In-Line Chiller-3,4 Condenser Water Split Standby Water 390 40 2.7 2.8 3 1750 No 6.5" CDWP-7 In-Line Closed Loop Freezer Condensers Split Duty Water 155 91 4.15 4.39 5 1750 No 9.125" CDWP-8 In-Line Closed Loop Freezer Condensers Split Standby Water 155 91 4.15 4.39 5 1750 No 9.125" CDWP-9 In-Line Open Loop Freezer Condensers Split Duty Water 425 48 3.67 4.75 5 1150 No 10.375" CDWP-10 In-Line Open Loop Freezer Condensers Split Standby Water 425 48 3.67 4.75 5 1150 No 10.375" HWP-1 Flr Mtd Heating Hot Water Split Duty Water 1410 110 28.3 30.2 40 1750 Yes 10.5" HWP-2 Flr Mtd Heating Hot Water Split Standby Water 1410 110 28.3 30.2 40 1750 Yes 10.5" HWP-3 In-Line HWC-1 Close Duty Water 41 19 0.2 0.22 0.25 1725 No 4.6875" HWP-4 In-Line AHU-6 Pre-heat coil pump Close Duty Water 165 14.9 0.48 0.6 0.75 1150 No 6" HWP-5 In-Line AHU-7 Pre-heat coil pump Close Duty Water 32 20 0.2 0.22 0.25 1725 No 4.6875" ERP-1 In-Line AHU-6 Energy Recovery Close Duty 30% Brine 185 55 2.2 3 3 1750 No 7.5" Mechanical Systems Existing Conditions Evaluation - 24 -

APPENDIX C SYSTEM FLOW DIAGRAMS Mechanical Systems Existing Conditions Evaluation - 25 -

Brine Solution Supply 20 Degree Cooler Fan Coil Units HWR 160 Degree HW Primary Pumps Gas Fired Boilers Brine Solution Return 25.8 Degree HW Secondary Pumps HWS 180 Degree Flow and Enthalpy Measuring Stations CDW Primary Pumps Outdoor Air Outdoor Air Temperature Monitoring Cooling Tower Water Cooled Brine Chillers CAV AHUS Hot Water Coils Chilled Water Coil F Duct Static Pressure Sensor VAV AHUS Hot Water Coils Chilled Water Coil F CDW Secondary Pumps Walk-in Freezer Condenser Water Heat Exchanger for Water Side Free Cooling Walk-in Freezer Condenser Water F F Return Air Supply Air Clothing Dry Storage Bulk Storage Staging Receiving CHWR 55 Degree Return Air VAV Box Supply Air Offices Dining Lockers Work Areas CHW Primary Pumps Water Cooled Centrifugal Chillers CHW Secondary Pumps (VFD) Walk-in Freezer Condenser Water Heat Exchanger for Over 50 degree Outdoor DBT Walk-in Freezer Water Cooled Condenser CHWS 45 Degree Overall HVAC Schematic

APPENDIX D ANNUAL ENERGY CONSUMPTION AND COST RESULTS INPUTS Figure D-1 Boiler performance characteristics Figure D-2 Chiller performance characteristics Mechanical Systems Existing Conditions Evaluation - 31 -

Figure D-3 Cooling tower performance characteristics Figures D-1 to D-3 indicated the performance characteristics of the major mechanical equipment used in the HAP energy analysis. Also, all major fan and pump efficiencies are used and taken from the design documents provided by H.F. Lenz Company. Fan efficiencies range from 45% - 74% Primary loop chilled water pump efficiency is 85% Secondary loop chilled water pump efficiency is 77% Mechanical Systems Existing Conditions Evaluation - 32 -

RESULTS Table D-1 Component Annual Cost Breakdown COMPONENT ANNUAL COST ($/YR) ANNUAL COST/FT 2 ($/FT 2 YR) % OF TOTAL ENERGY COST HVAC Component Air System Fans 21,303 0.242 2.7 % Cooling 23,239 0.263 2.9 % Heating 32,618 0.370 4.1 % Pumps 24,405 0.277 3.1 % Cooling Tower Fans 5,194 0.059 0.6 % HVAC Subtotal 106,759 1.210 13.4 % Non HVAC Component Lights 18,501 0.210 2.3 % Electrical Equipment 45,546 0.516 5.7 % Misc. Fuel Use 628,763 7.127 78.6 Non HVAC Subtotal 692,810 7.853 86.6 % TOTAL 799,569 9.063 100 % Table D-1 shows the annual energy cost to operate each component in the supply center. The table also breaks down the cost per square foot. Figure D-4 Annual component cost summary Mechanical Systems Existing Conditions Evaluation - 33 -

Figure D-5 Annual energy cost by fuel type Table D-2 Annual Energy Consumption Breakdown COMPONENT ANNUAL ENERGY CONSUMPTION HVAC Component Electric (kwh) 1,238,947 Natural Gas (therms) 23,969 Non HVAC Component Electric (kwh) 1,067,486 Natural Gas (therms) 464,855 TOTAL Electric (kwh) 2,306,433 Natural Gas (therms) 488,824 Aside from energy consumption, it is also important to recognize the amount emissions generated from operating the building. HAP also performs an annual emissions calculation for the production of CO 2, SO x, and NO x. Table 15 illustrates the estimated annual emissions produced for operating the supply center. Table D-3 Annual Emissions Report EMISSION CO2 SOx NOx AMOUNT PRODUCED 280,437 lb 652 kg 2,253 kg Figure D-5 and D-6 illustrate monthly cost to operate the supply center. D-5 is a breakdown according to each component where as D-6 breaks down the monthly cost by fuel type. Mechanical Systems Existing Conditions Evaluation - 34 -

Figure D-6 Monthly cost breakdown by component Figure D-7 Monthly cost breakdown by fuel type Mechanical Systems Existing Conditions Evaluation - 35 -